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    • 51. 发明申请
    • HEAT EXCHANGER
    • 热交换器
    • US20070131393A1
    • 2007-06-14
    • US11610203
    • 2006-12-13
    • Hironaka Sasaki
    • Hironaka Sasaki
    • F28B1/00
    • F28F9/0209F28D1/05391F28D2021/0073F28F1/022
    • A heat exchanger to be used as a gas cooler has a refrigerant inlet and a refrigerant outlet provided at upper and lower header sections, respectively, of a first header tank. A value represented by a formula {(L1+L2)/2}+(T×2N) is defined as an average flow path length L0, where L1 represents the total interior length of both the header sections of the first header tank, L2 represents the interior length of the header section(s) of the second header tank, T represents the length of the flat tubes, and N represents the number of the header section(s) of the second header tank. The positions of the refrigerant inlet and outlet are determined to satisfy the relation 0.8≦LX/L0≦1.2, where Lx represents a flow path length for refrigerant which flows into the upper header section from the refrigerant inlet and flows out of the refrigerant outlet.
    • 用作气体冷却器的热交换器具有分别设置在第一集水箱的上部和下部集管部分的制冷剂入口和制冷剂出口。 由式{(L 1 + L 2)/ 2} +(Tx2N)表示的值被定义为平均流路长度L 0,其中L 1表示第一集水箱的两个集管部分的总内部长度 ,L 2表示第二集水箱的集管部分的内部长度,T表示扁平管的长度,N表示第二集水箱的集管部分的数量。 制冷剂入口和出口的位置被确定为满足0.8 <= LX / L 0 <= 1.2的关系,其中Lx表示从制冷剂入口流入上集管段的制冷剂的流路长度,并流出 制冷剂出口。
    • 54. 发明授权
    • Heat exchange system and method
    • 热交换系统和方法
    • US06857467B2
    • 2005-02-22
    • US10361999
    • 2003-02-07
    • Raymond Lach
    • Raymond Lach
    • F28B1/02F28D7/00F28F27/02F28B1/00
    • F28D21/0017F28B1/02F28D7/005F28F27/02F28F2250/06
    • The heat exchange system is used for heating a first fluid with a second fluid, and includes a first fluid circuit comprising an upstream end, a downstream end and an intermediate portion therebetween and a second fluid circuit comprising an upstream end, a downstream end and an intermediate portion therebetween. The heat exchange system also includes a flooded heat exchanger unit wherein the intermediate portions of the first and second fluid circuits extend and are in adjacent, thermally-conductive contact for allowing heat transfer from the second fluid to the first fluid. The flooded heat exchanger is capable of being flooded in a determined proportion within the second fluid circuit intermediate portion. The heat exchange system further includes a second fluid circuit control valve located at the second fluid circuit downstream end, for controlling the flow rate of the second fluid through the second fluid circuit, whereby the proportion of the heat exchanger which is flooded within the second fluid circuit intermediate portion can be selectively calibrated. The heat exchange system also includes a first fluid pre-heating device located between the first fluid circuit upstream end and the heat exchanger unit, for partly pre-heating the first fluid before it is heated by the second fluid, whereby the first fluid temperature at the first fluid circuit downstream end will be stabilized.
    • 热交换系统用于加热具有第二流体的第一流体,并且包括第一流体回路,其包括上游端,下游端和中间部分,第二流体回路包括上游端,下游端和 中间部分。 热交换系统还包括淹没式热交换器单元,其中第一和第二流体回路的中间部分延伸并且处于相邻的导热接触件中,以允许从第二流体到第一流体的热传递。 淹水式热交换器能够在第二流体回路中间部分内以确定的比例淹没。 热交换系统还包括位于第二流体回路下游端的第二流体回路控制阀,用于控制通过第二流体回路的第二流体的流量,由此在第二流体内淹没的热交换器的比例 电路中间部分可以选择性校准。 热交换系统还包括位于第一流体回路上游端和热交换器单元之间的第一流体预热装置,用于在第一流体被第二流体加热之前部分地预热第一流体,由此第一流体预热装置 第一流体回路下游端将稳定。
    • 55. 发明授权
    • Rotating disk evaporative cooler
    • 旋转盘蒸发冷却器
    • US5974822A
    • 1999-11-02
    • US933946
    • 1997-09-19
    • William L. Kopko
    • William L. Kopko
    • F28C1/00F24F5/00F25B39/04F28B1/00F28D5/00F25D5/00
    • F25B39/04F24F5/0035F28B1/00F28D5/00F25B2339/041
    • A tank holds a pool of liquid coolant in which spaced, rotatable disks are partially submerged. An air flow is established over exposed portions of the disks, preferably parallel thereto, whereby coolant adhering to the disks upon rotating out of the coolant pool is partially evaporated and the disks and remaining adhering coolant have their temperature lowered and serve to cool the coolant pool upon reentry into the pool from the air space above. A fluid to be cooled is passed through tubes mounted in the tank, below the surface of the liquid coolant, parallel to the surfaces of the disks. Adjacent rows of tubes define spaces therebetween, each of which receives the submerged portion of at least one disk. The evaporative cooler may be used in a refrigeration apparatus in combination with a compressor and an evaporator.
    • 一个坦克装有液体冷却液池,其中间隔开的可旋转盘被部分浸没。 在盘的暴露部分上建立空气流,优选地平行于其中,从而在从冷却剂池旋出时附着到盘上的冷却剂被部分蒸发,并且盘和剩余的粘附冷却剂的温度降低并用于冷却冷却剂池 从上面的空气空间重新进入泳池。 要冷却的流体通过与液体冷却剂表面平行的盘安装在罐中的管道。 管的相邻行在其间限定空间,每个管接收至少一个盘的浸没部分。 蒸发冷却器可以与压缩机和蒸发器结合使用在制冷装置中。
    • 58. 发明授权
    • Integral blow down concentrator with air-cooled surface condenser
    • 具有风冷表面冷凝器的整体吹风浓缩机
    • US4969507A
    • 1990-11-13
    • US397725
    • 1989-08-23
    • Axel E. Rosenblad
    • Axel E. Rosenblad
    • F28B1/00F28D5/02
    • F28B1/00F28D5/02Y10S165/914
    • An evaporative condenser of the plate type having spaced heat exchange elements incorporates a blow down concentrator. Vapor enters the elements and after condensation therein by heat exchange with liquid flowing as a film on the outer surfaces of the elements; condensate is discharged from the bottoms of the elements. The coolant liquid is itself evaporatively cooled by a flow of cooling air passing outside the heat exchange elements, within a casing that encloses the elements. The cooling air may even be warmer than the coolant liquid so long as the air is not saturated. The overflow of cooling water from the condenser elements goes to the concentrator section, thus eliminating a separate piece of equipment especially dedicated to the concentrating of used coolant.
    • 具有间隔开的热交换元件的板式蒸发冷凝器包括吹出浓缩器。 蒸汽进入元件并在其中通过与在元件的外表面上作为膜流动的液体进行热交换而冷凝; 冷凝物从元件的底部排出。 冷却剂液体本身通过冷却空气流通过热交换元件外部,在围绕元件的壳体内进行蒸发冷却。 只要空气不饱和,冷却空气甚至可以比冷却剂液体更暖。 来自冷凝器元件的冷却水的溢出进入浓缩器部分,从而消除了特别专用于浓缩所用冷却剂的单独设备。